CN102600995B - Double-introduction-layer tower expanding cavity type separator - Google Patents
Double-introduction-layer tower expanding cavity type separator Download PDFInfo
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- CN102600995B CN102600995B CN201210060005.4A CN201210060005A CN102600995B CN 102600995 B CN102600995 B CN 102600995B CN 201210060005 A CN201210060005 A CN 201210060005A CN 102600995 B CN102600995 B CN 102600995B
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- 238000000926 separation method Methods 0.000 claims abstract description 39
- 238000004062 sedimentation Methods 0.000 claims abstract description 17
- 238000005192 partition Methods 0.000 claims 18
- 230000000712 assembly Effects 0.000 claims 1
- 238000000429 assembly Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 8
- 238000003756 stirring Methods 0.000 abstract description 6
- 230000000704 physical effect Effects 0.000 abstract description 4
- 239000007788 liquid Substances 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000012530 fluid Substances 0.000 abstract 2
- 230000010355 oscillation Effects 0.000 abstract 1
- 238000002156 mixing Methods 0.000 description 22
- 125000006850 spacer group Chemical group 0.000 description 19
- 239000000126 substance Substances 0.000 description 17
- 239000012071 phase Substances 0.000 description 7
- 239000006260 foam Substances 0.000 description 5
- 238000004945 emulsification Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 230000008676 import Effects 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 230000004308 accommodation Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 239000007790 solid phase Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000000693 micelle Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
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Abstract
The invention discloses a double-introduction layer tower expanding cavity type separator which can adapt to large production load variation and can not generate a phenomenon that bubbles are generated when high-speed gas-liquid stirring is carried out so that separation can not be carried out under high load. According to the invention, a unique double-introduction mechanism and multi-layer gradually-expanded separation chamber can ensure that even though the flow and physical property of a separation medium are greatly varied, the separator can adapt to the flow and the physical property; and by means of a Coanda effect namely wall-attached flow of fluid on an expanded wall surface, the fluid nearby a boundary deflects outwardly, axial symmetric circulation current with downward periphery and upward center can be naturally generated, thereby overcoming the self-sustained oscillation caused by clash impact of inner current in a pure cylinder chamber and reflect current at the bottom of the pure cylinder chamber. Multiple units of cyclone sedimentation separators can be combined and used, so that the separation space is saved, the separation efficiency is high, operation is stable, and the variable working condition adapting property is good. The double-introduction-layer tower expanding cavity type separator can be widely suitable for occasions such as oil-gas separation, water-gas separation, solid-liquid separation and dedusting separation.
Description
Technical field
The invention belongs to the centrifugal cyclone sedimentation-separation technology field of multi-phase ingredients, be suitable for gas-solid phase, liquid-solid phase containing solid particle, the liquid phase medium containing drop carries out efficient separation under the very large operating mode of its changes in flow rate scope.
Background technology
Decanter type and centrifugal rotary streaming separator are the multiphase separator patterns of commercial Application amount maximum.Decanter type relies on gravity to promote sedimentation and the floating of heavy, light phase, needs very large sedimentation face.Centrifugal rotary streaming relies on centrifugal force field to carry out brute force separation, and efficiency is higher.General decanter type separator (tank) often, with the centrifugation of entrance, makes heavy constituent attached to container inner wall sedimentation, light component make progress buoyance lift poly-in to outlet, then by filter, remove particle or the drop of sneaking into.And centrifugal rotary streaming separator is according to the difference of purposes, be often called cyclone separator, hydrocyclone etc.
Common decanter type separator, the heavy phase that contains a large amount of suspensions in its tank inner chamber body, rise heavy phase particle, so its volume is large, efficiency is low and flow can not excess load because the upflow velocity of lightweight phase can not blow.Horizontal sedimentation formula is slightly good, but still can not satisfy the demands.
Centrifugal rotary streaming separator, by means of powerful centrifugal force field, can make light, dense media fast hierarchical, has higher separative efficiency and production capacity.But, due to without the adding of moment of face, to defer under the prerequisite of the moment of momentum theorem, angular velocity of rotation and pressure between each layer of medium are inconsistent, and shearing turbulent flow and the eddy current of generation can make separating effect variation.In the situation that eddy flow is violent, can cause large micelle broken, stir and bear foam or produce emulsification, make medium be difficult to separation; The effect and eddy flow is too gently had no way of.Because tangential flow velocity is that swirl strength is directly proportional in the increase and decrease of flow, therefore generally very narrow corresponding to efficient separated treating capacity scope.
The situation that the load variations such as Oil-gas Separation are large or change field of employment for oil, gas field, often requires treatment facility to have large as far as possible operating flexibility.Adopt cut-out, the input operation of a plurality of equipment parallel connections not only to bother, also increase cost, if working conditions change is too frequent, does not catch up with operation and will be absorbed in failure state.
Summary of the invention
The present invention is just for the above-mentioned deficiency of existing separator, and a kind of brand new creating and action principle more effective " two introduced layer towers expansion cavate separator ", can overcome the deficiency of existing separator technology, greatly promote the variable working condition conformability of separator, and can dwindle significantly the volume of separator.
The invention provides a kind of structure is relatively simple, efficient, treating capacity changes accommodation very greatly, medium physical property strong adaptability, withstand voltage high separator, meet under oil, gas-field exploitation and other occasions, for gas-liquid separation, gas-solid and liquid-solid separated demand.
The innovative technology solution that the present invention takes is:
1. layer tower expanded the separation chamber of cavity structure
The present invention is divided into upper and lower two sections by the interior chamber of rotational flow settlement knockout drum (16), and what its main cyclone section (18) completed the layering of medium and dense media phase relies on flowing of inwall.And the rotational flow settlement section (17) of multilayer expansion, it is emphasis of the present invention, it has the structure of the multilayer expansion cavate as layer tower, by the conical cavity structure of expanding gradually, one section of cylindrical cavity is communicated to the cylindrical cavity of next section of enlarged-diameter, the conical cavity of formation cone post chamber in layer---i.e. one section of expansion is one section of cylindrical cavity of continued access again.The number of plies in cone post chamber is minimum be one deck, does not limit at most, and the diameter of lower one deck cylindrical cavity is greater than last layer, and each chamber all axially connects, and the bottom in last one deck cone post chamber is sealed.
Adopt above-mentioned structure, can play the effect of two aspects:
The first effect is the self adaptation that reaches treating capacity.When flow increases, the switching that binding medium imports, can flow in lower one deck cone post chamber by fast-descending, due to the increase of diameter, can significantly reduce swirl strength, can not stir foam and emulsification, and continue separated and attached wall sedimentation; And if flow continues to increase, medium also can flow in the cone post chamber that lower one deck diameter is larger by fast-descending, then reduces swirl strength, continue separated and attached wall sedimentation, the like.If treating capacity is less, medium just almost completes separation in last layer cone post chamber, then is deposited to cone post chamber below.
The second effect is to make separator working stability.Utilize the wall attachment effect (Coanda effect) of jet, inwall in flaring cone chamber, the axial flow of medium can be along cone chamber wall to extrinsic deflection, thereby avoid the rising discharge currents of light substance phase, produce downward along wall periphery, circulation in the chamber making progress along center, can make separator working stability, avoid as pure cylindrical cavity, in the medium in chamber, stream impacts with the contrajet head-on collision of bottom, causes self-oscillatory severe situation.
2. machine-processed corresponding to two importings of different flow
Separator of the present invention adopts two independently medium inlet and entrance cavities.Under low discharge, blending agent mostly from low discharge entrance (2) by low discharge surge chamber (6), enter and centripetal rotational flow generator (20), carry out strong pre-supination, tangential inflow in rotational flow settlement knockout drum (16) carried out centrifugal and sedimentation separation, because flow is little, the tangential velocity flowing into is limited, swirl strength is also suitable, can not stir and bear foam or produce emulsification.And when treating capacity increases, by outside stream, regulate and control, blending agent passes through large flow surge chamber (4) from the large flow entrance (1) on top mostly, enter in axial rotational flow generator (22) and carry out suitable prewhirling, under spiral, flow to again in rotational flow settlement knockout drum (16) and carry out centrifugal and sedimentation separation, because flow is large, the tangential velocity that spiral enters is still higher, enough cyclonic separation, and the axial flow velocity of spiral flow, can make medium drop to quickly in the cone post chamber that lower one deck diameter is larger, avoid the time to grow and stir raw foam, treating capacity with automatic increase separator.
3. multiunit any parallel connection and parts shares
Separator of the present invention also adopts the topology layout of a plurality of separative elements application in parallel, each rotational flow settlement separative element is by rotational flow settlement knockout drum (16) separately, the prewhirl axial rotational flow generator (22) of large flow blending agent, the prewhirl centripetal rotational flow generator (20) of low discharge blending agent, light substance delivery line (15), the parts such as dense media leadout hole (14) form, axial rotational flow generator (22) is installed on the upper surface of upper spacer (5), upper spacer perforate () is opened in the position that upper spacer (5) covers at axial rotational flow generator (22), centripetal rotational flow generator (20) is contained between upper spacer (5) and median septum (7), median septum is opened median septum perforate (19) in the hollow position place of centripetal rotational flow generator (20) correspondence, axial rotational flow generator (22), centripetal rotational flow generator (20), the perforate of two dividing plates all with rotational flow settlement knockout drum (16) the centering center of circle.Structure like this, the parts such as each rotational flow settlement separative element can common media entrance, outlet, surge chamber, membrane support, and all needn't bear pressure medium, and therefore can save a large amount of material costs and space, the pressure of medium relies on the shell (3) of separator to bear.
The invention has the beneficial effects as follows:
1. can significantly promote the changes in flow rate accommodation of separator, the high efficiency range of separative efficiency is broad, and operating flexibility is large, need to frequently not regulate from outside.
2. in separator, be difficult for stirring raw foam and emulsification, the strong adaptability of separator to medium physical property.
3. drag losses is little, and the treating capacity of unit volume equipment is large.
4. save material, easy to manufacture, can bear high-pressure medium, be adapted to especially the separation of high-pressure oil gas.
Below in conjunction with the drawings and specific embodiments, the present invention is described further.
Accompanying drawing explanation
Accompanying drawing 1 is the overall construction drawing of the two introduced layer tower expansion of the present invention cavate separator.
Accompanying drawing 2 is in each rotational flow settlement separative element of separator of the present invention, the structure chart of the centripetal rotational flow generator (20) of the low discharge blending agent of prewhirling.
Accompanying drawing 3 is in each rotational flow settlement separative element of separator of the present invention, the first version of the axial rotational flow generator (22) of the large flow blending agent of prewhirling---the structure chart of the axial rotational flow generator (22) realized by axial diversion prerotation vane.
Accompanying drawing 4 is in each rotational flow settlement separative element of separator of the present invention, the second version of the axial rotational flow generator (22) of the large flow blending agent of prewhirling---the structure chart of the axial rotational flow generator (22) realized by spiral grooves shaft part ().
Referring to accompanying drawing 1, the two introduced layer tower expansion of the present invention cavate separator comprises shell (3), upper spacer (5), median septum (7), lower clapboard (9), large flow entrance (1), the large flow surge chamber (4) that upper spacer and shell upper surround, low discharge entrance (2), upper and in the low discharge surge chamber (6) that surrounds of two dividing plates and shell upper portion, the dense media that in lower two dividing plates of neutralization and shell, lower portion the surrounds chamber (8) of confluxing, dense media outlet (10), the light substance that lower clapboard and outer casing underpart the surround chamber (11) of confluxing, light substance outlet (12), with at least one rotational flow settlement separative element institute.For each rotational flow settlement separative element, mainly by rotational flow settlement knockout drum (16), tank underseal closing plate (13), the axial rotational flow generator (22) of the large flow blending agent of prewhirling, the parts such as the centripetal rotational flow generator (20) of the low discharge blending agent of prewhirling, light substance delivery line (15), dense media leadout hole (14) separately, formed.Wherein axial rotational flow generator (22) is installed on the upper surface of upper spacer (5), and upper spacer perforate () is opened in the position that upper spacer (5) covers at axial rotational flow generator (22); And centripetal rotational flow generator (20) is arranged between upper spacer (5) and median septum (7), median septum is opened median septum perforate (19) in the hollow position place of centripetal rotational flow generator (20) correspondence.Upper and lower rotational flow settlement section (17) two parts that are divided into main cyclone section (18) and multilayer expansion in interior chamber of rotational flow settlement knockout drum (16), main cyclone section (18) is cylindrical cavity, or one section of cylindrical cavity continued access is shunk conical cavity and then is connect cylindrical cavity, and the rotational flow settlement section (17) of multilayer expansion is up-small and down-big layer turriform, the structure of every one deck is that cone post chamber---i.e. the conical cavity of one section of expansion is one section of cylindrical cavity of continued access again, cone post chamber the number of plies minimum be one deck, do not limit at most; The diameter of lower one deck cylindrical cavity is greater than last layer, each chamber all axially connects, the bottom in last one deck cone post chamber is sealed by tank underseal closing plate (13), the middle part vertical plug-in mounting light substance delivery line (15) of tank underseal closing plate (13), derived score from after light substance to the light substance chamber (11) of confluxing; At the periphery of tank underseal closing plate (13) or the periphery bottom in last one deck cone post chamber, open dense media leadout hole (14), derived score from after dense media to the dense media chamber (8) of confluxing.
Referring to accompanying drawing 2, the prewhirl centripetal rotational flow generator (20) of low discharge blending agent, by being an assembly being formed by the centripetal runoff blade of multi-disc (24), blade is arranged by radial, is installed under runoff blade pressed on ring support plate (23) and runoff blade and encircles between support plate (25).
This assembly is installed between upper spacer (5) and median septum (7), the circle diameter at blade outer rim place is greater than median septum pod apertures () footpath, under the distribution circular diameter of blade inside edge and blade pressed on ring support plate (23) inner circle opening diameter, runoff blade, encircle support plate (25) inner circle opening diameter close, three center of circle alignment, blade be shaped as straight plate shape, or crooked, twisted shape.
Low discharge blending agent is the excircle of centripetal rotational flow generator (20) from this assembly, inwardly enter the runner between centripetal runoff blade (24), be subject to the guide functions of blade, become rotating flow, tangentially enter the inferior upper space in rotational flow settlement knockout drum (16), start eddy flow and sedimentation separation.
Referring to accompanying drawing 3, the axial rotational flow generator (22) of the large flow blending agent of prewhirling, the assembly that one of its version is comprised of multi-disc spiral axial blade (27), blade is arranged by radial, is installed in blade sleeve (26).
This assembly be axial rotational flow generator (22) be installed on centripetal rotational flow generator (20) above, i.e. the upper surface of runoff blade pressed on ring support plate (23), and the center of circle of aliging with it.The diameter of blade sleeve (26) is more than or equal to the inner circle opening diameter of blade pressed on ring support plate (23), blade be shaped as distortion or prismatic blade, along the hand of spiral rotation of blade sleeve (26) inner circle, tilt to install.
Large flow blending agent enters the runner between spiral axial blade (27) from the upper port of blade sleeve (26), be subject to the guide functions of blade, become axial screw stream, the dirty upper space entering in rotational flow settlement knockout drum (16), starts eddy flow and sedimentation separation.
Referring to accompanying drawing 4, the prewhirl axial rotational flow generator (22) of large flow blending agent, two of its version is by screw sleeve (28), and jacket is also fixedly mounted with the assembly that screw rod shaft part (29) that its circumferential surface is processed with single-screw groove or many spiral grooves forms.
This assembly be axial rotational flow generator (22) be installed on centripetal rotational flow generator (20) above, it is the upper surface of runoff blade pressed on ring support plate (23), and the center of circle of aliging with it, the diameter of screw sleeve (28) is more than or equal to the inner circle opening diameter of blade pressed on ring support plate (23).
Large flow blending agent enters the spiral grooves of screw rod shaft part (29) and the helical flow path that sleeve lining surrounds from the upper port of screw sleeve (28), be subject to its guide functions, become axial screw stream, the dirty upper space entering in rotational flow settlement knockout drum (16), starts eddy flow and sedimentation separation.
The specific embodiment
Below in conjunction with drawings and Examples, the present invention is elaborated, but be not limited to the present embodiment.
As shown in Figure 1, the two introduced layer towers expansion of the present invention cavate separator, be the large flow surge chamber 4 that surrounded by shell 3, upper spacer 5, median septum 7, lower clapboard 9, large flow entrance 1, upper spacer and shell upper, low discharge entrance 2, upper and in lower portion surrounds in lower two dividing plates of low discharge surge chamber 6, neutralization that surround of two dividing plates and shell upper portion and shell dense media confluxes that chamber 8, dense media export 10, lower clapboard and outer casing underpart surround light substance conflux chamber 11, light substance export 12 and at least one rotational flow settlement separative element form.Wherein: each rotational flow settlement separative element is comprised of rotational flow settlement knockout drum 16, tank underseal closing plate 13, the axial rotational flow generator 22 of the large flow blending agent of prewhirling, the parts such as the centripetal rotational flow generator 20 of the low discharge blending agent of prewhirling, light substance delivery line 15, dense media leadout hole 14 separately; Axial rotational flow generator 22 is loaded on the upper surface of upper spacer 5, upper spacer perforate 21 is opened in the position that upper spacer 5 covers at axial rotational flow generator 22, centripetal rotational flow generator 20 is contained between upper spacer 5 and median septum 7, and median septum is opened median septum perforate 19 in the hollow position place of centripetal rotational flow generator 20 correspondence.On the interior chamber of rotational flow settlement knockout drum 16, under be divided into rotational flow settlement section 17 two parts of main cyclone section 18 and multilayer expansion, main cyclone section 18 is cylindrical cavity, or one section of cylindrical cavity continued access is shunk conical cavity and then is connect cylindrical cavity, and the rotational flow settlement section 17 of multilayer expansion is up-small and down-big layer turriform, the structure of every one deck is that cone post chamber---i.e. the conical cavity of one section of expansion is one section of cylindrical cavity of continued access again, cone post chamber the number of plies minimum be one deck, do not limit at most, the diameter of lower one deck cylindrical cavity is greater than last layer, each chamber is all axially to connect, the bottom in last one deck cone post chamber is sealed by tank underseal closing plate 13.The middle part vertical plug-in mounting light substance delivery line 15 of tank underseal closing plate 13, rotational flow settlement knockout drum 16 and the light substance chamber 11 of confluxing is communicated with, at the periphery of tank underseal closing plate 13 or the periphery bottom in last one deck cone post chamber, open dense media leadout hole 14, last one deck cone post chamber and the dense media chamber 8 of confluxing is communicated with.
Axial rotational flow generator 22 in each rotational flow settlement separative element, centripetal rotational flow generator 20, corresponding upper spacer perforate 21, median septum perforate 19 all with the rotational flow settlement knockout drum 16 centering centers of circle separately.
In low discharge situation, blending agent enters separator from low discharge entrance, by low discharge surge chamber 6, enter again in one or more centripetal rotational flow generator 20 simultaneously, by the runner between centripetal runoff blade 24 wherein, produce and prewhirl, enter again the inferior upper space of corresponding rotational flow settlement knockout drum 16, start eddy flow and sedimentation separation.
Under heavy traffic condition, blending agent enters separator from large flow entrance, by large flow surge chamber 4, enter again in one or more axial rotational flow generator 22 simultaneously, by one of flow passage structure form between spiral axial blade 27 wherein), or the groove runner version of the screw rod shaft part 29 by wherein two), become axial screw stream, the dirty upper space entering in corresponding rotational flow settlement knockout drum 16, starts eddy flow and sedimentation separation.
The cylindrical cavity of each different inner diameters of rotational flow settlement knockout drum 16 inner chambers is by the conical cavity connection transition of corresponding upper and lower cylindrical cavity respectively of two ends internal diameter, the inside diameter ranges of each cylindrical cavity is between 4～2500 millimeters, draw ratio scope is 0.1～10, the interior cone angle of conical cavity is between 2～150 °, the ratio of the internal diameter in two-layer adjacent column chamber is between 1: 1.02～1: 2, and the thickness of rotational flow settlement knockout drum 16 walls is between 0.2～30 millimeter.
At the bottom of tank, the light substance delivery line 15 of plug-in mounting imports lower clapboard by light substance after separation and confluxes in chamber 11 with the light substance that outer casing underpart surrounds, then from dense media outlet 10 outflows.During dense media leadout hole 14 imports dense media, dense media that in lower two dividing plates and shell, lower portion surrounds confluxes in chamber 8, then from dense media outlet 10 outflows.
The height of light substance delivery line 15 is between 1～600 millimeter, and diameter is between 1～300 millimeter, and height is between 5～3000 millimeters.The diameter of dense media leadout hole 14 is between 1～300 millimeter.
As shown in Figure 2, layer tower expansion cavate rotational flow settlement separator of the present invention, in each rotational flow settlement separative element, the prewhirl centripetal rotational flow generator 20 of low discharge blending agent, be one by the centripetal runoff blade 24 of multi-disc, by radial, arrange, be installed under runoff blade pressed on ring support plate 23 and runoff blade and encircle the assembly forming between support plate 25, this assembly is installed between upper spacer 5 and median septum 7, the opening diameter that encircles support plate 25 inner circles under the distribution circular diameter of blade inside edge and blade pressed on ring support plate 23 inner circles and runoff blade is close, three center of circle alignment, the quantity of centripetal runoff blade 24 is 2～30, thickness is 0.1～20 millimeter, blade be shaped as straight plate shape, or crooked, twisted shape, blade outer rim place's tangent line and arrange diameter to angle α between-45 °～+ 45 °, inner edge place tangent line and angle β are radially between 0 °～90 °.
As shown in Figure 3, layer tower expansion cavate rotational flow settlement separator of the present invention, in each rotational flow settlement separative element, the prewhirl axial rotational flow generator 22 of large flow blending agent, one of its version is by multi-disc spiral axial blade 27, by radial, arranges, be installed in interior the formed assembly of blade sleeve 26, this assembly be installed on centripetal rotational flow generator 20 above, i.e. the upper surface of runoff blade pressed on ring support plate 23, and the center of circle of aliging with it.The diameter of blade sleeve 26 is more than or equal to the inner circle opening diameter of blade pressed on ring support plate 23, between 3～1500 millimeters, 2～30 of spiral axial blade 27 quantity, 0.2～20 millimeter of thickness, blade be shaped as distortion or prismatic blade, hand of spiral rotation along blade sleeve 26 inner circles tilts to install, and the inclination angle γ of blade outer rim and sleeve axis is between 1 °～88 °.
As shown in Figure 4, layer tower expansion cavate rotational flow settlement separator of the present invention, in each rotational flow settlement separative element, the prewhirl axial rotational flow generator 22 of large flow blending agent, two of its version is by screw sleeve 28, jacket is also fixedly mounted with the assembly that screw rod shaft part 29 that its circumferential surface is processed with single-screw groove or many spiral grooves forms, this assembly be installed on centripetal rotational flow generator 20 above, it is the upper surface of runoff blade pressed on ring support plate 23, and the center of circle of aliging with it, the diameter of screw sleeve 28 is more than or equal to the inner circle opening diameter of blade pressed on ring support plate 23, between 3～1500 millimeters, the lead of screw angle of screw rod shaft part is between 10 °～80 °, length is between 4～1500 millimeters.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210060005.4A CN102600995B (en) | 2012-03-08 | 2012-03-08 | Double-introduction-layer tower expanding cavity type separator |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210060005.4A CN102600995B (en) | 2012-03-08 | 2012-03-08 | Double-introduction-layer tower expanding cavity type separator |
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| CN102600995A CN102600995A (en) | 2012-07-25 |
| CN102600995B true CN102600995B (en) | 2014-04-02 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU220790U1 (en) * | 2022-09-14 | 2023-10-03 | Владимир Александрович Лаптев | Filter-separator for cleaning the coolant of the external circuit of marine internal combustion engines |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105749823B (en) * | 2014-12-16 | 2018-06-29 | 中国科学院大连化学物理研究所 | A kind of low residence time gas-liquid reactor |
| CN104524825A (en) * | 2015-01-15 | 2015-04-22 | 福建德兴节能科技有限公司 | Efficient cyclone separation device and method |
| CN113007067A (en) * | 2021-04-26 | 2021-06-22 | 珠海格力电器股份有限公司 | Silencer and compressor |
| EP4584026A1 (en) * | 2022-09-05 | 2025-07-16 | Luxnara Yaovaphankul | A cone stack cyclone separator and vacuum cleaner having same |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3672502A (en) * | 1970-03-27 | 1972-06-27 | Polysius Gmbh | Apparatus for purifying dust loaded waste gases |
| DE3009214A1 (en) * | 1980-03-11 | 1981-09-17 | Friedrich Wilhelm Dörrenberg Wirtschaftliche Verbrennungs-Technik, 5063 Overath-Untereschbach | Centrifugal dust separator - with spiral cyclone inlet and spiral guide plates on central dip tube |
| CN101828088A (en) * | 2007-08-22 | 2010-09-08 | 特兰斯朗科技有限公司 | Gas liquefaction and separation apparatus |
| CN202516704U (en) * | 2012-03-08 | 2012-11-07 | 大连理工大学 | Double lead-in layer tower expansion cavity type separator |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FI20010570L (en) * | 2001-03-20 | 2002-09-21 | Fortum Oyj | Method and separation device for separating two phases from each other |
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2012
- 2012-03-08 CN CN201210060005.4A patent/CN102600995B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3672502A (en) * | 1970-03-27 | 1972-06-27 | Polysius Gmbh | Apparatus for purifying dust loaded waste gases |
| DE3009214A1 (en) * | 1980-03-11 | 1981-09-17 | Friedrich Wilhelm Dörrenberg Wirtschaftliche Verbrennungs-Technik, 5063 Overath-Untereschbach | Centrifugal dust separator - with spiral cyclone inlet and spiral guide plates on central dip tube |
| CN101828088A (en) * | 2007-08-22 | 2010-09-08 | 特兰斯朗科技有限公司 | Gas liquefaction and separation apparatus |
| CN202516704U (en) * | 2012-03-08 | 2012-11-07 | 大连理工大学 | Double lead-in layer tower expansion cavity type separator |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU220790U1 (en) * | 2022-09-14 | 2023-10-03 | Владимир Александрович Лаптев | Filter-separator for cleaning the coolant of the external circuit of marine internal combustion engines |
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| CN102600995A (en) | 2012-07-25 |
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